Apparatus for producing carbonblack



May 4, 1937. .J. J. JAKOSKY ET AL APPARATUS FOR PRODUCING CARBON BLACK Original Filed March 31, 1935 5 SheetsSheet l .53; Euqq 052mg M0 910 Eur:

T HD INVENTORS: John J. JAKOSKY, we OR F. HANSON,

' ATTORNEY INVENTORS: JOHN J.J -\KosKY, VICTOR F: HAnso XEADQ NEE/OD s Sheets-Sheet 2 m UENZQZ J. J. JAKOSKY ET AL APPARATUS FOR PRODUCING CARBON BLACK Original Filed March 51, 1935 A TTORNEII/ BY n May 4, 1937.

mumnnuun n24 wmuzdism EU: or 046 :0 POI May 4, 1937. J. J. JAKOSKY ET AL APPARATUS FOR PRODUCING CARBON BLACK 1953 5 Sheets-Sheet 3 Original Filed March 31 all!!!"all"filf"llflflflla ui H m INVENTORJ':

JOHN J- JAKO5K BY \/\CTOR r=- HAHson,

ATTORNEY May 4, 1937. J. J. JAKOSKY ET AL.

APPARATUS FOR PRODUCING CARBON BLACK Original Filed March 31, 1933 5 Sheets-Sheet 5 a liquid by electrothermal"dissociation or other Patented May 4, 1937 APPARATUS FOR PRODUCING CARBON- BLACK John J. Jakosky, Los Angeles, Calif., and Victor F. Hanson, Niagara Falls, N. Y., assignors to Electroblacks, Inc., Culver City, Calif., a corporation of Nevada Original application March 31, 1933, Serial No. 663,790. Divided and this application October 17, 1935, Serial N0. 45,451

15 Claims. (Cl. 204--31) This invention relates to the production of carbon-black, and particularly to methods involving the production of carbon-black in suspension in an organic or carbon-bearing liquid medium, as for example by electrothermal dissociation of such a liquid, and the separation of the carbon-black from such liquid medium by evaporation, and to apparatus in which such production and separation may be carried out.

This application is a division of our co-pending application Serial Number 663,790, filed March 31, 1933.

The invention may be considered as comprising an apparatus for heat-treating a mixture of carbon-black and an organic liquid, such as an oil, to effect a substantially complete separation of liquid and other impurities from the carbonblack and produce a carbon-black having certain characteristic properties which render it especially advantageous for certain purposes, such as rubber compounding. Such method of treatment may be applied either to a mixture of carbonblack and organic liquid obtained by the direct production of carbon-black in suspension in such separation, evaporation (following concentration of the carbon-black by settling, filtration or the like), or by extraction with a suitable solvent.

Although various methods of separating carbon-black from oil suspensions have been proposed, it has been found that the only practical, and satisfactory method for removal of the last portion of liquid from the carbon-black is by evaporation. The methods heretofore proposed have required that the carbon-black be subjected to a separate mechanical separating operation such as centrifuging, filtering, or settling, prior to the evaporation or thermal drying operation.

An object of the invention is to provide a method and apparatus therefor in which the necessity for mechanical concentration of the carbon-black-liquid-mixture is eliminated, by so conducting the process that the liquid separation may be effected entirely by evaporation, without requiring the furnishing of a prohibitively large amount of heat for this purpose.

In addition to other disadvantages 'the abovementioned methods hitherto disclosed .for production of a liquid-free carbon-black have been found unsuited to the production of carbon-black of the most advantageous properties for use in the rubber trade. The extraction method produces a rubber black which possesses the proper physical and chemical characteristics, but this method of separation has not been found economically feasible. Partial separation of the carbon-black from the liquid medium by filtration or centrifugal treatment must necessarily be followed by a more complete separation, such as by evaporation or extraction, and the cost is much higher than in the process of the present means, or to a mixture prepared by mixing an impure or inferior carbon-black or lamp-black product with a suitable organic liquid, the principal purpose of the treatment in the latter case being to alter or improve the properties of the black and obtain a superior grade of carbonblack having more desirable characteristics for certain purposes.

According to a preferred embodiment, however, the invention also comprises a complete apparatus for production of carbon-black by subjecting .an oil or other carbon-bearing liquid to electrothermal treatment to produce carbonblack by dissociation of a portion of such liquid, causing such carbon-black to accumulate in suspension in another portion of such liquid to form a carbon-black-liquid-mixture of suitable concentration, and then subjecting such mixture to thermal treatment as above described for the product-ion of a liquid-free substantially pure carbon-black of advantageous properties.

According to the methods ofproduction of carbon-black by electrothermal dissociation of carbon-bearing liquids hitherto proposed, particularly as exemplified in Jakosky Patent 1,597,277 and Jakosky Patents 1,673,245 and 1,872,297, the carbon-black was produced in a liquid medium consisting principally of carbonbearing liquid from which the carbon-black was subsequently removed by filtration, centrifugal when certain type oils are treated for the production of carbon-black, a filtration or centrifuging step prior to evaporation causes a compacting of the carbon-black particles so that, upon ultimate drying of these particles, a carbon-black is produced which is quite difilcultly milled into rubber; a serious disadvantage as regards the use of the material in rubber compounding.

Removal of the residual liquid by previously proposed methods of direct evaporation from the carbon-black-oil-mixture, or of evaporation from a concentrated mixture obtained by filtration or centrifugalmeans', has been found impractical for the production of the higher quality blacks, for the reason that the residual carbon-bearing liquid is in part caused to sinter" the carbonblack particles together, forming relatively dense coked" particles or agglomerates of carbon which invention. Furthermore, it has been found that,

cannot be properly dispersed when milled into rubber.

In the methods heretofore proposed for drying a mixture of carbon-black and oil by evaporation, the drying operation necessarily extends over a considerable period of time. This results in the formation of considerable quantities of gum and resinous materials. It has been found that this percentage of gum can be greatly reduced by making the drying time as short as possible. Another factor which influences the percentage of gugn formed may be termed the surface. or contact effect. It has been found that gum formation is increased when an unsaturated oil is evaporated to dryness in contact with the heated walls of a metal container and/or with large masses of carbon-black at high temperature. Tests have shown that this percentage of gum can, therefore, be reduced by employing two conditions during the drying operation: (1) a rapid or instantaneous. evaporation of a relatively large proportion of the oil from the black; and (2) minimizing the contact of the oil being evaporated, or the liberated vapors, with the retort walls or the partially dried black.

An important object of this invention, therefore, is to provide a method and apparatus for effecting substantially complete separation of oil or organic liquid from carbon-black, by evaporation, under such conditions as to cause extremely rapid or flash evaporation of a considerable portion of such liquid and to also minimize contact of the liquid or the vapors thereof with heated walls or with heated masses or particles of carhon-black, and thus minimize the formation of gums or other polymerization products during such operation.

Furthermore, the presence of oxygen, during the drying operation, also tends to increase the formation of gums or other objectionable polymerization products. In addition, the presence of oxygen or oxygen-bearing gases during the drying operation and the subsequent cooling of the black is objectionable due to the tendency of the carbon-black-to take up or adsorb such oxygen or oxygen-bearing gases, which detract from the properties of the black, particularly when compounded with rubber, it having been found that such adsorbed oxygen or oxygen-bearing gases tend to cause deterioration of rubber.

Consequently a further object of the invention is to provide a complete process and apparatus for production of carbon-black by electrotherrnal dissociation, and subsequent removal of liquid and cooling 'of the dried black, under conditions of substantial exclusion of oxygen. A further important object of the present invention is to produce a carbon-black of admirable characteristics for use as a filler, particularly in rubber compounding, by a method involving separation of the carbon-black from the residual liquid and other undesirable constituents in such manner that the advantageous properties of such black with respect to such use thereof are preserved.

A further important object of the present invention is to provide a method for the production of carbon-black characterized by its substantial freedom from adsorbed or condensed gums, cementing materials, coking agents and hydrocarbons, and by its ease of proper dispersion by milling into rubber.

A further object of the invention is to provide apparatus in which the method of the present invention may be practiced, whereby the advanor suspension of carbon in the remaining liquid is then subjected to a rapid evaporating operation at reduced pressure, to separate said remaining liquid from said carbon by evaporation thereof at a pressure lower than that maintained during such dissociation, and preferably at a pressure not in excessof atmospheric, to produce substantially pure, liquid-free carbon in the physical state commonly referred to as carbon-black.

The above-mentioned dissociation may be carried out by maintaining an electric arc discharge between electrode submerged within a body of such liquid, and the evaporation of the remaining liquid from the carbon is preferably effected largely or wholly by flash-evaporation obtained by discharge of the mixture of carbon and liquid, while still at a high temperature, from the superatmosphericpressure under which the dissociation is conducted, into a drying chamber main- :1

tained at relatively low pressure. This flashevaporation step may be followed by a further heating operation for the purpose of removing residual volatiles or liquids, if any, which may be present in said carbon-black after such fiashevaporation.

The dissociation step is preferably conducted under such temperature and pressure conditions as to provide for flash-evaporation of substantially all or a major portion of the residual carhon-bearing liquid from said carbon-black by the agency of the sensible heat of said liquid and said black, whereby a relatively small amount of additional heat is required for complete drying of said black following said flash-evaporation step.

Another important feature of the invention is that the dissociation of the carbon-bearing liquid may be carried out under conditions which allow for maintenance of high concentration of carbon-black in the liquid, which has hitherto been unattainable without excessive heat losses;

According to this invention the electrothermal dissociation is preferably continued until a concentration of between 5 and per cent of carbonblack by weight is obtained in the carbon-blackliquid-mixture, and the mixture is maintained during such dissociation under a sufliciently high pressure to permit substantially all'of the heat delivered to the liquid by the electrothermal dissociation means to be retained in the liquid without causing excessive vaporization thereof in spite of the relatively low throughput of the liquid which is necessary to provide this relatively high concentration, and the heat thus retained in the oil is subsequently utilized in the evaporation of the remaining liquid from the mixture. After completion of the drying and heat treatment of the carbon-black; said black is subjected to a cooling operation, preferably in an enclosed chamber.

Another important feature of the invention is that the heat treatment of the black following flash-evaporation iscarried out under conditions of progressively increasing temperature, and the vapors evolved during the flash evaporation and during said heating operation are removed from the carbon-black in such manner as to prevent contact of said vapors with carbon-black particles, or with heated wall surfaces, which are at a higher temperature than said vapors. This result may be attained, for example, by passing the carbon-black, following flash-evaporation, longitudinally through a drying chamber of progressively increasing temperature, and withdrawing evolved vapors longitudinally of said chamber in a direction opposite to the direction of travel of the carbon-black. If desired, the vapors may be positively removed from the chamber adjacent the position of evolution thereof, as by means of a perforated vapor outlet pipe extending longitudinally within the drying cham- -ber.

The process of the present invention is preferably carried out under conditions which provide for substantially complete exclusion of oxygen, this being accomplished by maintaining the liquid undergoing dissociation, as well as the carbonblack in all the stages of production, in an atmosphere consisting principally of gases evolved by the electrothermal dissociation, or other oxygen-free gases. Such oxygen-free gases will be referred to hereinafter as inert gases. It has further been found desirable in some cases to conduct the drying and cooling steps of the carbon-black production cycle in the presence of a counter-current stream of such an inert gas, whereby removal of volatiles from the carbonblack may be facilitated by a reduction of the partial pressure of such volatiles during the drying step and the carbon-black may be protected from contact by oxygen-containing gases during the cooling step.

The cooling procedure may, if desired, include the introduction of a suitable treating agent in vapor form to the cooling black so that said black is caused to cool in the presence of such an agent, as and for the purpose hereinafter set forth.

The above-described method is preferably carried out continuously, by continuously supplying a carbon-bearing liquid to the dissociation chamber and continuously removing the carbon-blackliquid-mixture therefrom and subjecting the same to flash-evaporation followed by heating and cooling, as above-described, and the gaseous dissociation products formed by the dissociation reaction (which may comprise hydrogen, methane, acetylene or the like) are preferably also continuously withdrawn from the chamber iii and passed in heat exchanging and scrubbing relation to the in-coming liquid, in such manner that the sensible heat of such gaseous products is utilized in heating such liquid, and in such manner that any carbon-black or condensable carbon-bearing liquid products carried by such gaseous products will be caused to enter the incoming liquid stream and be thus returned to the dissociation chamber.

The carbon-black produced by the method herein described is characterized by certain physical properties, such carbon-black being preferably obtained in the form of small loosely bonded aggregates of carbon particles which may be readily crushed or milled into an impalpable powder, but which are possessed of sufficient physical strength to allow reasonable handling thereof without excessive flying or floating of the finer particles. The carbon-black obtained by practice of the present invention is particularly characterized by a definite vesicular or honey-comb structure of the individual aggregates above referred to.

The apparatus of the present invention comprises means for carrying out the above-described operations including dissociation of carbon-bearing liquid to produce a carbon-black-liquid-mixture and the subsequent steps of flash-evaporation, heating and cooling to recover the carbonblack from such -mixture. Said apparatus will be more fully described hereinafter.

The accompanying drawings illustrate one form of apparatus in accordance with this invention, and in which the method of the present invention may be carried out, and referring thereto: I

Fig. 1 is a diagrammatic representation of one form of apparatus which may be used for practice of the complete invention;

Fig. 2 is a vertical section, partly in elevation, of the dissociation chamber and dryer-feed portions of the apparatus, on an enlarged scale;

Fig. 3 is a sectional detail of the form of carbon-black treater or dissociation chamber shown in Fig. 2, taken on line 3-3 therein;

Fig. 4 is a sectional detail of an alternative form of feeding device for the dryer;

Fig. 5 is a partly sectional side elevation of the drying apparatus shown diagrammatically in Fig. 1;

Fig. 6 is a transverse section thereof, taken on line 66 in Fig. 5;

Fig. 7 is an enlarged sectional detail of the means connecting together the upper and lower sections of the dryer;

Fig. 8 is a partly sectional elevation of an alternative form of apparatus adapted for carrying out the flash-evaporation step of the present invention;

Figs. 9 and 10 are sectional details thereof, taken on lines 9-9 and Ill-Ill, respectively, in Fig. 8;

Fig. 11 is a partly sectional elevation of an alternative form of dryer means, in which the drying operation is divided into three separate stages; 7

Fig. 12 is an enlarged sectional detail of the upper end portion of the first stage of the dryer shown in Fig. 11;

Fig. 13 is a transverse view taken on line" referred to as oil), connected by a conduit to a scrubber and heat exchanger 2 which is in turn connected to an electrothermal d ssociation chamber 3 by means of an oil conduit 30. and a vapor conduit 3?). Said scrubber is adapted to receive gases from the chamber 3 through the conduit 32) and heat the oil supplied to said chamber from the storage receptacle I, so that most effective utilization of the thermal energy in these gases may be had and at the same time cause the principal proportion of condensable vapors in said gases to be absorbed in the entering oil stream and'returned to the dissociation Mixture, and abbreviated CBOM") is passed under pressure and at an elevated temperature to the inlet end of a suitable kiln-dryer 5, into which it is flashed" and the principal proportion of the liquid allowed to evaporate substantially instantaneously. The kiln 5 is preferably of the rotary .tube type and is provided with means for applying additional heat to the flashed carbonblack, in such manner that'the partially dried carbon-black is allowed to progress from the inlet end into and through a progressively hotter drying zone or section 3| and thence through a cooling zone or section 32 into a suitable receiving hopper 6. Suitable means such as a screw conveyor 1a may be provided for removal of the cooler carbon-black from the hopper 6 to suitable storage means I, from which it may be withdrawn by conveying means lb and delivered to suitable packaging means, if desired. The

- present invention also contemplates subjecting the cooling carbon-black to the action of a suitable treating agent, subsequently described, and provision is made, as at 8, for the introduction of such agent.- A suitable inert gas may also be introduced at 8 to facilitate removal of the volatiles from the carbon-black.

The vapors resulting from the flash-evaporation of the CBOM and the subsequent drying of the carbon-black are withdrawn from the kiln adjacent the inlet end thereof as' at 9, and are passed to a cooling condenser I, wherein the condensable portions of such vapors are separated and returned to the oil supply means, for example through the conduit l2 to the line 2a, and the non-condensable gases are passed through conduit lb to the gasometer. In some cases, the liquid collected in condenser may contain a liquid other than the condensed oil vapors; for example, if a treating agent is introduced at i] which is immiscible with the condensed carbon-bearing liquid, and in such cases, a suitable separator I3 may be connected to conduit l2, for example, as shown, to provide for separation of any such immiscible liquid. In the event that it is considered desirable to operate the dryer 5 at a subatmospheric pressure, a suitable pump ll may be connected in the vapor line coming from the condenser II. It may also be found desirable to provide a suitable pump in the conduit 2, for 3 example as shown at |2a, to facilitate return of as for example by means of a conduit 90 leading from the conduit 0 to the conduit SD. A suitable pump 9!) is preferably provided in the conduit in to facilitate transfer of the vapors from the conduit 9 to the conduit 3b.

It may also be found desirable or convenient to provide a pump in the line leading from the oil storage through the heat exchanger to the dissociation chamber, so that oil may be con-.

tinuously forced into said chamber independent of the pressure maintained therein. This pump may be located in the oil line 2a entering the heat exchanger, as at l5, or this pump may be put in the oil line 3aadjacent the dissociation chamber 3 if desired.

Figs. 2 and 3 show the dissociation chamber 3 in more detail. Said apparatus is shown as being of the type shown and described in the pending application of Jakoslny, Serial No. 588,146 and comprises essentially a casing or container 2| provided with a plurality of electrode units mounted within said casing and each comprising a relatively fixed and one or more relatively movable electrodes, there being, inthe form shown, three of such units, indicated at E1, E2 and Ea. I

Each electrode unit may comprise a relatively fixed ring-shaped electrode 22 whose upper face 220 constitutes an arcing face formed as a surface of, revolution, of relatively small width in proportion to its circumferential length, and

lying in a plane substantially perpendicular to its axis, and a relatively rotatable electrode holder 23 mounted on a rotatable shaft 24 and having one or more radial arms 23a each carrying a rod-shaped electrode 25 of relatively small cross-section disposed above the corresponding electrode surface 22a and inclined rearwardly with respect to the direction of travel of said electrode at a suitable trailing angle. The electrodes 22 and 25 may be formed of any suitable conducting material; for example, such electrodes may advantageously consist of carbon and may be manufactured in the same general manner as other carbon electrodes commonly employed for maintaining electric arcs. Power supply to the respective electrodes may comprise suitable connection to the several electrodes whereby electrical energy at the desired potenlate the ring electrodes 22 from the casing 2| and connect these electrodes each to aseparate phase of a three-phase power supply system, which maycomprise a suitable transformer T, through suitable reactances R and R? or the like, while connecting the rotating electrodes to ground as at G through the common shaft upon which they are mounted, through the casing 2|, as shown in Fig. 2.

It will be understood that suitable driving means, for example, a variable speed motor 24a, are provided whereby rotation of the shaft 2 may be had, and that adjustment means such as is indicated at 2"), are provided for determining, maintaining and adjusting the separation of the rotatable electrodes from the fixed electrodes through longitudinal movement of the shaft 24. The above mentioned means, for the purpose of the present description, may be substantially as shown and described in the above referred to pending application, Serial No. 588,146. 7

At the concentrations of carbon-black contemplated in the present invention, it is dlfllcult to accurately govern by means of a valve the feed of the CBOM from the dissociation apparatus to the drying apparatus. Means are therefore provided for properly controlling this feed, and the form of feed-control means shown herein may comprise one or more montejus devices such as indicated at 26 and 21, provided at their lower ends with connection as at 260. and 21a to the dissociation chamber 3, and at their upper ends with pressure fluid connections 26b and 21b. The above-mentioned connections are provided with suitable valves indicated by prime marks on the respective reference numerals, as at 26a, etc. A line 28 connected to the bottom of both of the montejus devices through valved connections 28a and 28b leads to the inlet end of the dryer 5. The montejus devices 26 and 21 may be provided with valved vents 26c and 210 at their upper ends.

When it is desired to feed CBOM into the dryer, one of the montejus devices, for example 26, is filled with CBOM from the dissociation chamber 3 by opening the valve 26a, with the valves 21a, 28a, and 2671 closed. As the pressure in the dissociation chamber forces the CBOM into the montejus, the vent 260 may be cracked slightly so as to allow the montejus to fill, and the vent valve 260 and valve 26a then closed. The valve 26?) is then opened to the desired degree to admit a suitable pressure fluid, such as a compressed hydrocarbon gas, to the montejus 26, and the valve 28a opened to allow the CBOM. to be forced out through the line 28 to the dryer. While the montejus 2a is being emptied into the dryer, the montejus 21 may be filled as above described, and the respective montejus devices may be alternately operated, so that a substantially continuous withdrawal of CBOM from the dissociation chamber 3 and a substantially continuous supply of CBOM to the dryer is maintained.

The dryer 5 may comprise an. elongated tube inclined downwardly from the inlet to the outlet end, provided with external heating means for the upper or inlet end portion, said heating means being preferably so disposed as to provide a zone of continuously increasing temperature downwardly from the inlet end to the lower end of said portion. The dryer, as shown in Figs. '5 to 7, may comprise an upper or heating section 3|" and a lower, or cooling section 32. -I'he upper section 3| is preferably of greater cross-sectional area than the lower section 32, so that the car ,bon-black in descending through the upper secsaid black is obtained, while causing the carbonblack to occupy a relatively large proportion of the cross-sectional area of the lower section 32, thereby assuring better contact between the material and the dryer walls to facilitate transfer of heat from the black to said walls, andbetter contact between the black and the treating vapor or gas which may be passed upwardly through said lower section, as subsequently described. The upper section 3| is provided with heating means which may comprise a burner 33 directed into a fire-box 34 provided with a heating chamher or flue 35 built around the section 3| and having a stack 36 at the upper end thereof. This construction provides for maintaining a downwardly increasing temperature in the heating section 3| in such manner that the carbon-black descending through said section is exposed to continuously increasing temperature during its downward passage from the inlet end to the lowe e d,

of said section. The dryer may be rotatably mounted on suitable bearings 31a, 31b and 310, which may rest on suitable supports 38.

Referring particularly to Figs. 2 and 4, the upper end of the upper section 3| is provided with a tubular extension 39, preferably of reduced diameter, on which is mounted a sprocket 4| through which the dryer may be rotated by means of a chain 42 and a motor 43. Said extension 39 extends within a fixed housing or vapor outlet chamber 44, provided with a vapor outlet connection 9 leading to the condenser N (Fig. 1). The CBOM supply line 28 is connected to an inlet pipe 46 which extends longitudinally through housing 44 and extension 39, said inlet pipe preferably terminating within the upper end portion of the dryer section 3|. in position to discharge the CBOM into said section, preferably toward the side-walls thereof, as by means of a nozzle shown at 41. The chamber 44 is preferably also provided with a vapor-tight connection with the tubular extension 39, as by means of a stuffing-box 48.

The CBOM feeding means shown in Fig. 4 may, if desired, be used in place of the plain nozzle 41, so that a gas relatively inert at the temperatures involved, may be used to atomize the CBOM into the dryer. This alternative form of feeding means may comprise an atomizing gas line 50a extending longitudinally through the housing 44 and the tubular extension 39 and provided with a discharge nozzle 50?) at its inner end, and a CBOM discharge line 50c extending within said line 50a and terminating adjacent said nozzle. This arrangement provides for introduction of CBOM into the dryer through the discharge line 500 simultaneously with the introduction of atomizing gas through the nozzle 50b, whereby said CBOM is atomized in its introduction to the dryer.

If desired, a super-heated gas may be introduced to the CBOM discharge line 28 at any suitable pointfor example such as at 28c, as shown in Fig. 2. It will be comprehended that any suitable type of gaseous agent may be introduced in this manner, for example, hydrogen, methane, or other suitable gas, such as that produced during the dissociation of the oil and con sisting in general of a mixture of hydrogen and gaseous hydrocarbons. be introduced at this point, although we prefer, in general, to use an oxygen-free gas.

As shown in Fig. 5, the lower end of the dryer may be provided with a suitable hopper 5, to receive the dried carbon-black, the hopper being conveniently provided with a clean-out manhole 6a whereby the black may be removed at intervals, as desired. A suitable form of packing or stufling-box means 6b is preferably provided for the hopper, so that escape of gases from the dryer can be prevented. It will beunderstood that a suitable continuous discharge means such as is shown at la in Fig. 1 may alternatively be provided for the hopper, if desired, for continually removing material from said hopper and conveying the same to a storage receptacle 1. An inlet pipe 8 may be provided, extending upwardly a short distance into the lower section 32 for in troduction of a treating agent or inert gas into the drying zone.

At the junction of the sections 3| and 32, where a change in diameter of the two sections takes place, suitable means are provided for causing the dried carbon-black to enter the tube 32 in such manner as to prevent accumulation of dried In some cases, steam may black in contact with the side walls of the heating section at the lower end thereof. Such means, as shown in Figs. to 7, may conveniently comprise a bailie plate 3la disposed diametrically across the lower end of the section 3| and two oppositely inclined scoop-plates 3lb and lie disposed at opposite sides of the plate Ma. The

rotation of the dryer (in the direction indicated by the arrow in Fig. 6) will cause the scoop-plates to gather such dried black as may fall into the lower portion of the apparatus at the point indicated by the arrow Z and lift the same through a portion of a revolution of the dryer and then cause the black to pass by gravity into the upper end of section 32.

Fig. 7 shows a flexible coupling device 5| which may be provided for the purpose of securing the respective dryer sections 3| and 32 together during rotation of the dryer, while taking care of any eccentricities in the alignment of said sections due to heating effects. Said coupling means may comprise a spherical bearing member 52 secured to the upper end of the section 32 disposed within a housing 53 secured to and projecting axially from the end of the section 3| and provided at its outer end with a flange 53a, said housing and said bearing member 52 being secured together frictionally by means of packing material 54 which is kept under compression by means of a flange 55 bolted to the flange 53a, so that upon rotation of the section 3| by means of the motor 43, the frictional engagement of the between the section 32 and the end of the section 3i as at 56, and between the flange 55 and the section 32, as at 56c, so as to accommodate any misalignmentof the one section with respect to the other section. The bearing 31a at the lower end of the section 32 may be of such construction as to take up any thrust in said section, and preserve the longitudinal position of said section, while the upper bearing 31b on section 32 and the bearing 31c on section 3i may be allowed to float so that longitudinal expansion of the dryer will occasion no bearing difllculty. As the dryer expands the tubular extension 39 may slide with respect to the housing 44, through the stufllngbox 48.

In one method of practicing the present invention, a carbon-bearing liquid such as, for example, kerosene, Edeleanu extract, or other suitable liquid, (any such liquid being generally referred to herein as an "oil")', is placed in the storage receptacle I and a supply of this oil is conveyed to the dissociation chamber 3 through the heat exchanger 2. As above mentioned, a suitable pump or the like may be placed in this oil supply line so as to provide supply of oil to the dissociation chamber under any operating pressure established in said chamber. With the electrodes 22 and 25 properly energized, an electric arc will be established between the arcing surfaces of said electrodes, causing dissociation of the carbon-bearing liquid or oil.- This dissociation results in the formation of carbon-black in the liquid body in finely dispersed state and also results in formation of fixed gases such as acetylene, methane, hydrogen, and other gases, which 4 for storage.

The electric arcs within the dissociation chamber 3 evolve considerable heat,and the heat thus evolved is utilized to increase the temperature of the liquid body within the chamber to a suitable super-atmospheric temperature. According to the preferred embodiment of the present invention, the mixture of carbon-black and dissociable liquid is maintained under a superatmospheric pressure within the dissociation chamber, sufficient to prevent boiling of the liquid at the temperature of operation, which temperature is preferably about equal to or in excess of the boiling point of the heaviest fractions of the liquid, at the pressure at which the subsequent flash-evaporation is conducted.

When a dissociable liquid such as kerosene is used for production of carbon-black according to the present invention it has been found practical to maintain a gauge pressure of 50 lbs. per sq. in. on the dissociation chamber, which pressure will allow of an average temperature of in the neighborhood of 500 F, to be attained by the CBOM within the treater without excessive gasimixture, the upper limit of this concentration being limited principally by the fluidity of the mixture. In general, the liquid is preferably caused to remain in the dissociation apparatus until the concentration of carbon-black therein has reached-approximately the maximum value consistent with the above mentioned limitations. When kerosene is used as the dissociable liquid, this concentration may conveniently reach approximately l3% carbon-black under the tem-' perature and pressure conditions above outlined,

while concentration above this amount has been found to cause surface leakage on insulators within the dissociation chamber.

When a suitable concentration of carbon.- black has been attained in the mixture within the dissociation chamber, this mixture may be withdrawn from the treater and introduced to one of the montejus devices 25 or 21, and fresh oil introduced to the treater, it being understood that the rate of withdrawal of the CBOM'and the rate of supply of fresh liquid to the treater may be so balanced as to maintain a substantially continuous flow of liquid to and CBOM from this treater.

Referring to Fig. 2, when one montejus is filled with CBOM to the desired extent, the valves 26a, 26b, 26c, 21a, 21b, 210, 28a and 28b are properly set so as to obtaindelivery of CBOM from the montejus to the dryer, suitable fluid pressure being applied to the montejus so as to force the CBOM through the inlet line 28. It will be understood that the CBOM is preferably maintained under the above mentioned superatmospheric temperature and pressure conditions up to the moment of discharge thereof into the dryer section 3| and the montejus devices and the necessarysupply pipes may be provided with suitable insulation for this purpose. When the CBOM is discharged into the dryer, which is maintained at a relatively low pressure preferably not in excess of atmospheric, the mixture will flash, causing a vaporization of the major portion of the volatile matter in said mixture.

It will be comprehended that, dependent upon the concentration of carbon-black and the temperature and pressure atwhjch the mixture is "flashed, the degree of vaporization of the volatile constituents of said mixture may be controlled within rather wide limits. It has been found disadvantageous to-cause a complete vaporization of said constituents in the flashing operation for the reason that the carbon-black thus obtained is in the form of a very fine, almost impalpable powder, which is not only difiicult to collect butis not preferredby the rubber trade inasmuch as it is very disagreeable to handle. In order to produce a carbon-black, therefore, which is properly dried yet in suitable physical condition, the present invention particularly contemplates flashing the CBOM under such temperature and pressure conditions and at such carbon-black concentration that the flash evaporation thereof results in the formation of lumps or loosely-bound agglomerates of carbon-black particles and a very small proportion of dust or substantially none at all. According to the preferred method of drying the CBOM, these loosely bound agglomerates have a "honey-comb or vesicular appearance and structure similar to that of lava or other material which has solidified while evolving gases or which contained considerable quantities of gas during solidification. This honey-combstructure of the dried material allows it to be broken down with very slight mechanical pressure and this feature is of particular advantage in providing for better incorporation and dispersion of the material in rubber. The size of these agglomerates is preferably maintained on the order of a few millimeters in diameter, for example from 0.75 to 10 mm. in diameter.

When the mixture is flashed under such conditions as to produce lumps of the size and type above described it has been found desirable to subject the same to a further drying operation to remove the residual liquid and gaseous material. According to the preferred form of the invention. therefore, the CBOM produced as above outlined is flashed into a suitable heating zone under such conditions as to produce the above described lumps and therein and thereafter exposed to sufliclent additional heating to completely remove the major proportion of volatiles therefrom.

When a dryer of the type herein disclosed is used, the CBOM is flashed into the upper section 3| and is allowed to pass downwardly through this section upon rotation thereof after the manner of the well known types of rotary dryers. Heat is applied to the exterior of this section of the dryer and the carbon-black is gradually brought to a temperature suflicient to drive out the volatile constituents. The temperature of the black at the lower end of the dryer section 3| may advantageously be as high as 1300 F. One of the particular features of this type of dryer is that the flashed carbon-black is moved downwardly through the dryer and is gradually brought to maximum temperature, while the gaseous products are driven upwardly past the descending black in such manner that these bases are caused to contact carbonblack and surfaces which are at a lower temperature than that of the gases whereby decomposition of these gases by such contact is minimized to a great degree, minimizing formation of the aforementioned condensation or polymerization products which cause a sintering of the material,

After passing through the dryer section 3| the black is fed into the dryer section 32 by means of the arrangement shown in Figs. 6 and 7 and is progressively cooled during its passage through said section 32, and then discharged into the hopper from which it may be withdrawn to storage or packaging as desired.

The CBOM may be mixed with other materials before introduction into the dryer system, if desired, for example the CBOM may be flashed into the dryer by atomization thereof with a suitable atomizing gas, an arrangement such as shown in Fig. 4 being used for this purpose. This arrangement obtains a better evaporation of the liquid constituents of the CBOM, particularly in lowering the partial pressure of such constituents. In addition to assisting the evaporation, the presence of such gas appears to be advantageous in preventing undesirable caking at the CBOM discharge.

In addition to the above described means for assisting the evaporation of the liquid constituents from the CBOM, the flash-evaporation and subsequent-heating may be carried out under such conditions as to maintain a reduced partial pressure of the said volatile constituents during the evaporating steps, which condition may be obtained by maintaining a subatmospherie pressure within the dryer or by passing a suitable inert-gas through said dryer by introduction of such a gas at 8, and establishing a stream of such gas through and over the drying black.

The form of apparatus shown in Figs. 8 to 10 t is adapted to provide for a concentration of the h CBOM obtained in the dissociation chamber 3 in a combined flash-evaporating and filtering step. The filter portion of this form of device is a modification of a continuous filter" such as thatshown and described in Reissue Patent to J T. Shimmin No. 18,597, in which a plurality of filter surfaces are arranged to receive spray-discharged CBOM and obtain. further concentration by filtration. Referring to the above-mentioned figures, the numeral 60 indicates a filter housing rotatably mounted as at El and 62 on suitable supporting means and provided with rotating driving means 63; the filter housing 60 is provided with a plurality of filter sections 64 disposed circumferentially around the inner periphery of said housing and each provided with a suitable supporting structure such as a screen 65 carrying a filter medium such as a woven wire cloth filter surface 66. Each of the filter sections 64 is provided with connections 61 leading from the space behind the filter support 65 and connecting to a conduit 68. The several conduits 68, the number of which corresponds to the number of filter sections Bl, are brought readily inwardly of the filter housing and lead into an axially projecting housing portion a and thence longitudinally of the apparatus to and through a manifold plate 69, which forms an end plate for the housing portion 60a. A valve plate Ill is provided adjacent the plate 69 and a cap member 60b is provided on the end of the housing portion 60a adapted to hold the valve plate H1 in position with respect to the plate 59. The valve plate is provided with valve openings 10a and 10b adapted to register with the open ends of the pipes 68 and connections II and 12 are provided extending through the cap member filter through the cap member 60b, being provided with a suitable stuffing-box as shown at 16, and is provided within the housing Gil with a radially extending portion 15a having a longitudinally extending portion 15b disposed at a suitable distance radially inwardly of the fllter tion 64. As these filter sections pass the nozzles c a suction is applied thereto through the conduits 69 which are in communication with the connection II through the valve openings Illav and this suction will obtain a removal of a portion of the unfiashedliquid content of the CBOM, which is drawn off through the connection II and may be returned to the dissociation chamber 3. After the filter sections have passed through a suitable proportion of a revolution of the housing 69, for example through an arc such as indicated at F1 in Fig. 9, the conduits 68 are disconnected from the suction line H and are connected to the suction line I2 through the valve opening 10b, and the portion of the revolution of the filter indicated at F2 is utilized in the removal of gas from the interior of the filter 69 so as to maintain the same under sufficiently low pressure to provide the desired flashevaporation. This gas may consist of fixed gases resulting from the dissociation step and vaporized constituents of the CBOM. The above described filtering operation results in the formation of a layer of carbon-black containing a materially low percentage of liquid constituents, and thislayer is removed from the filter surface 66 as by means of a stripper or scraper I1 and caused to fall into a hopper18, directed into a screw conveyor I9 and removed from the filter into a conduit 80 which is directed into suitable stufling box means being provided as at- 84 to obtain proper sealing of the rotating upper end of the dryer tube with the vapor duct. It will be understood that suitable sealing means are provided for sealing the screw-con veyor to the filter, so that atmospheric air is not drawn into said-filter, and mixed with the hydrocarbon and other gases therein. The filter housing 50 may be provided with an end plate 60, and the housing carrying the portions of the screw-conveyor which are exterior of the filter may be provided with striding-box means 69" at the point of passing through said end plate, to effect such sealing. It will be further understood that the entirev filter housing 69 rotates with respect to the conveyor I9, and said conveyor passes rotatably through the end plate 50 and may be rotatably supported at the other end of said housing as at 190..

The form of dryer shown in Figs. 11 to 14 is a modification of the form of dryer shown at 5 in Figs. 1 and 5, and comprises, essentially, a relatively low-temperature heating stage designated as Stage I, a relatively high-temperature heating stage designated as Stage II, and a cooling stage designated as Stage III. Stage I of the dryer may comprise an inclined tube 86 rotatably mounted in a heating chamber 81 and provicled.with CBOM feeding means at the upper end thereof and carbon-black discharging means at the lower end thereof. The CBOM feeding means may comprise a conduit 88 extending downwardly into said tube through a fixed housing 89 mounted on the upper end of said tube in such manner as to provide a vapor seal therewith and at the same time permit rotation of the tube 86. At a suitable point within the tube- 36, the conduit 88 may terminate in a CBOM discharge nozzle No, such point being preferably adjacent the upper end of the heating chamber 81. The lower end of the tube 36 may open into a suitable hopper 9I in position to discharge carbon-black thereinto, a suitable vapor-sealing means being provided at the point of entrance of said tube to said hopper, such as a stufling box 92.

The hopper 9| is adapted to deliver carbonblack downwardly into the Stage II, which may comprise a tube 93, provided at one end with a portion 94 of reduced diameter, and the hopper 9| may be provided with a spout opening into the portion94. The tube 93 is provided with a screw-conveyor 96 having driving means 91 and adapted to carry the carbon-black from the por tion 94 through the length of the tube 93 to the other end thereof, at which point a conduit 98 leading to Stage III is disposed. Stage III may comprise a tube 99 provided with a reduced portion I III after the manner of the portion 94 of the tube 93, and the conduit 98 is so disposed as to open into said portion IIII. The tube 99'is provided with a screw-conveyor after the man-- ner of the tube 93, Fig. 14 showing the construc-.

tion of this conveyor in the vicinity of the reduced portion IUI in greater detail. The screw conveyor, may comprise a portion I02 of large diameter fitting within the tube 99 and provided with an extension III3 of reduced diameter and decreased pitch fitting within the portion IIII. The particular arrangement shown is for the purpose of providing a relatively slow feed of carbon-black from the conduit 98so that the reduced portion IIII may be maintained substantially fullof such carbon-black while providing relatively faster feed of such carbonrblack through the tube 99, so that such black will only partially fill the cross-section of said tube. The

above described feeding arrangement is also pref 4 vapor through the several stages, and such means may comprise a conduit I04 leading into' the discharge end of the tube. 99 through which a ,suitable vapor or gas may be admitted, which gas will pass through the tube 99 and thence outwardly thereof through a conduit I95 connected through a heater I06 disposed in the fire-box IIl'Iof the heating chamber 81 to a conduit I98 communicating with the discharge end of the tube 93. A conduit I09 leads from adjacent the inlet end of the tube 93 to storage, or other disposition. A by-pass conduit III] is connected into the line I05 at a suitable point, and is led into the lower or discharge end of the tube 86, said conduit extending through the hopper III and upwardly into said tube 86 to adjacent the position of the upper end of the heating chamber 81 and there terminates in a closed end, for example as shown at IIIlb in Fig. 12. The portion of the conduit III) lying within the tube 86 is provided with a series of perforations IIOa adapted for discharge of vapor into said tube. Means are provided for removal of gas from the tube 86, and such means may comprise a conduit III having a closed lower-end Ila extending from adjacent the lower end of the tube 06 upwardly through said tube alongside the conduit IIO. as shown in Fig. 13 for example, and outwardly through the fixed housing 99. This conduit may be connected to any suitable storage means, such as the gasometer 4, as desired. The portion of the conduit lying within the tube 86 is provided with a series of perforations IIZ extending from adjacent the closed lower end upwardly to a point preferably somewhat above the point of CBOM discharge. The proportional dimensions of the conduits II 0 and III with respect to the diameter of the tube 66 is preferably such as to allow sufficient room for the carbonblack to descend through said tube. If desired, the two conduits H0 and III may be disposed upwardly of the axial line of the tube 86 rather than axially of said tube. The two conduits are preferably provided with guard or baffle means such as a plate II3 disposed over said conduits in such manner as to prevent accumulation of carbon-black thereon.

In the operation of the form of dryer above described, the tube 86 is externally heated by heat delivered from the fire-box I 01, provided with a burner or the like H0. The heated gases from the fire-box are directed to the lower end of the tube 86, as by means of a duct MM, and are passed in contact with said tube upwardly toward the inlet end thereof through the heating chamber 81, and are discharged adjacent the upper end of said heating chamber through a suitable flue H5. The particular heating arrangement shown herein is for the purpose of providing means for progressively heating of the tube 86 downwardly from the inlet to the discharge end thereof.

Rotation of the tube66 is obtained by suitable driving means, for example such as is shown at Al, 42 and in Fig. 2 in connection with the dryer 5. and CBOM is supplied through the conduit 88 and discharged into the heated and rotating tube 06 at the nozzle 88a. The CBOM is flash-discharged into the tube and the carbon-black is gravitated downwardly through the tube to the discharge end due to the downward inclination and rotation of said tube. The carbon-black is discharged from the tube 86 into the hopper 9I and falls through the conduit 95 into the portion 90 of the tube 93, is carried through said tube 93 by the action of the conveyor 96 and fed into and carried through the tube 99 in the same manner as in the case of tube 93. A suitable cooling gas or vapor, such as the gas resulting from the dissociation chamber, is passed at a relatively low temperature into the discharge end of the tube 99 through the conduit I04 and is passed through the tube 99 in counter-current contact with the hot carbon-black. In this contact, the gas is materially heated and the carbon-black materially cooled; the cooled carbon-black being discharged from the tube 99 into a suitable hopper II5, from.which it may be removed as desired by means of a conveyor II6 to suitable packaging means, not shown.

The gas which is passed through the tube, 99 in heat-interchanging relation to the hot "carhon-black, is withdrawn from said tubethrough the conduit I05 and, a portion thereof is led like.

increased through the heater I06 and thence through conthrough conduit IIO into the tube 86, suitable valve means being provided as at I05a and I05b in the respective conduits I05 and H0 whereby the proportional amounts of such gas are delivered to the desired portions of the apparatus. The portion of the gas passed through the heater I06 is heated to a relatively high temperature and is introduced into the discharge end of the tube 93 and passed there-through in heating contact with the carbon-black presenttherein, after which said' gas may be delivered through conduit I09 to storage or other disposition. The portion of the gas passed into the tube 86 obtains a reduction of the partial pressure of the volatiles released from the carbonblack undergoing heating in said tube, and is removed through the conduit III to storage or the The gas and vapors withdrawn from both drying tubes 86 and 93 may be introduced to the conduit 3b (Fig. 1) leading from the dissociation chamber 3, if desired, after the manner of the conduit 91:. leading from the dryer 5, whereby condensible vapors may be recovered therefrom and the heat economies described in connection with the first-described form of apparatus may be realized.

The flash-discharged carbon-black is subjected to heat applied exteriorly of the tube 86 whereby the temperature of said black is gradually increased during its downward passage through said tube, and in addition to the heating obtained in the above manner, the heated gas passed into the tube 66 through the conduit IIO also obtains a degree of heat-interchange with said black and serves particularly to facilitate the removal of the principal proportion of the volatiles from said black by a reduction of the partial pressure thereof. Considerable drying of the black is obtained in the tube 86, but it is preferable that the temperature in this stage be kept somewhat below the maximum temperature required for complete drying, in order to minimize the for-' mation of polymers or "cementing materials as above described. For example, the temperature of the black in Stage I may be kept' below about 700 or 800 R, if desired, so as to provide for evaporation and removalof the major portion of the liquidwlnder conditions which preclude heating thereof to an excessively high temperature, and the black may then be raised to a higher temperature in Stage 11, under conditions gas passed in cooling relation with the hot black in Stage III and then passed through the heater I06 may be heated to any desired temperature in said heater, this operation cooling the burner gases in the fire-box I01 so that said burner gases will contact the tube 86' at a somewhat lowered temperature.

The drying operation is thus seen to be divided into three distinct stages: in Stage I the CBOM is flash-discharged into a heated zone and caused to give up the major portion of its volatiles in the presence of a counter-current stream of gas made possible by the present process, it will be,

adapted to lower the partial pressure of such volatiles and assist in the removal thereof; in Stage II the carbon-black is further heated and the final portions of volatiles removed therefrom entirely through the agency of a heated gas passed counter-currently therewith; and in Stage III, the carbon-black is cooled through the agency of a counter-current stream of gas and the thermal energy of said black utilized in raising the thermal energy of said gas, which is further utilized as above set forth.

The carbon-black is thus constantly maintained in a desired atmosphere, namely that of an inert gas, whereby the desirable characteristics of such carbon-black are preserved. At no time, from the moment of formation of said black until the packaging thereof, is it possible for any deleterious atmosphere. such as air for example, to come into contact with the black, and the cooling of the black in the presence of a desired atmosphere will cause the black to adsorb and become saturated with undeleterious vapors, whereby there is small tendency for subsequent adsorption of any other vapor or gas, such as oxygen, during handling of the black.

The above drying procedure also provides advantageous economies in fuel consumption in addition to the economies set forth in connection with the operation of the dryer 5, particularly in that the sensible heat of the hot carbon-black is utilized in heating the treating gas during the passage thereof through Stage III. It will be further appreciated that any desired type of treating agent may be introduced to the black in Stage III, such as pine-tar-oil, stearic acid or the like.

' The present invention contemplates operation of a full cycle of carbon-black production under such thermal conditions as to produce a maxi-' mum quantity of dried and commercially marketable carbon-black with a minimum outlay of electrical and heat energy. This may be carried out by maintaining the temperature and pressure on the dissociation chamber at the highest values consistent with safe operating procedure, utilizing this temperature and pressure to cause evaporation of the carbon-black oil mixture, recovering the condensible vapors from the above mentioned evaporation, and returning such condensed vapors to the liquid supply line. The gas withdrawn from the dissociation chamber is caused to give up the principal proportion of its thermal,

energy in raising the temperature of the liquid supplied to the dissociation chamber.

As compared to previous methods of electrothermal production of carbon-black, the efficiency of the complete dissociation and drying cycle of the present invention is materially increased by virtue of the fact that heat impartedto the liquid undergoing dissociation in the dissociation chamber is more completely retained in such liquid instead of being dissipated by re-circulation and cooling of said liquid, so that said liquid is maintained at a materially higher temperature than has been hitherto employed. As a result, a small er proportion of the'heat evolved by the dissociation means is consumed in raising the temperature of the oil from the temperature of the oil body to the dissociation temperature, and the thermal energy stored in the carbon-black-oil mixture is utilized in the subsequent fiash-evapo ration of the remaining liquid. 7 v

In addition to the heat and energy economies further appreciated that the present process eliminates the objectionable filtration or solventextraction step required by previously disclosed methods. The advantages in this saving are tremendous from the standpoint of labor, and cost of equipment.

We claim:

1. An apparatus for producing carbon-black comprising: an inclosed dissociation chamber;

means for supplying liquid to said dissociation chamber and for maintaining a superatmospheric. pressure therein; electrode means within said chamber for creating an electric arc to heat said liquid and cause dissociation thereof; an

enclosed drying chamber; conduit means leading from said dissociation chamber to said drying chamber; means forheating material within said drying chamber, said heating means being adapted to heat liquid material entering said drying chamber substantially at the point of en-.

trance so as to cause rapid-evaporation of said liquid material, means for removing vapors from said drying chamber and for maintaining a condition of reduced pressure therein with respect to ,the pressure in said dissociation chamber;.

and means for removing solid material from said drying chamber. I

2. An apparatus for producing carbon-black comprising: an inclosed dissociation chamber;

chamber, said conduit means opening into said drying chamber through flash-discharge nozzle .means; means fo'r heating material within said drying chamber and for maintaining a condition of reduced pressure therein with respect to the pressure in said dissociation chamber; and means for removing solid material from said drying. chamber.

3. An apparatus for producing carbon-black comprising: an inclosed dissociation chamber;

.means for supplying liquid to said dissociation chamber and for maintaining a superatmospheric pressure therein, electrode means within said chamber, forcreating an electric arc to heat said liquid and cause dissociation thereof; an enclosed drying chamber; conduit means leading from said dissociation chamber to 'said drying chamber; means for heating material within said drying chamber; means for removing vapors from said drying chamber and for maintaining a condition of reduced pressure therein with respect to the pressure in said dissociation chamher; and means for removing solid material from said drying chamber; said apparatus also comprising heat exchanging and scrubbing means in said liquid supplying means adapted for countercurrent contact of liquid flowing to said dissociation chamber with vapor'flowing from said drying chamben 4. An apparatus for producing carbon-black comprising: an inclosed dissociation chamber; means for supplying liquid to said dissociation chamber, arcing electrode means within said disscciation chamber; in inclosed drying chamber comprising a longitudinally extending housing; conduit means leading from said dissociation chamber and opening into said drying chamber the material within said drying chamber to progressively higher temperature in the direction of said longitudinal movement; means for removing vapors from said drying chamber; and means for discharging solid material from said other end of the drying chamber.

5. An apparatus as set forth in claim 4, and also comprising means for introducing inert gas into said drying chamber.

6. An apparatus as set forth in claim 4, and also comprising means for introducing an inert gas into said drying chamber adjacent said other end thereof.

7. An apparatus as set forth on claim 4. said vapor removing means being so disposed and connected to the interior of said drying chamber as to remove vapors evolved from material passing therethrough without permitting such vapors to contact material within said drying chamber at a higher temperature than that at which said vapors are evolved.

8. An apparatus as set forth in claim 4. said vapor removing means communicating with said drying chamber adjacent the same end as said conduit means.

9. An apparatus as set forth in claim 4, said vapor removing means communicating with said drying chamber adjacent the same end as said conduit means and said apparatus also comprising means for introducing an inert gas into said drying chamber adjacent the opposite end thereof.

10. An apparatus as set forth in claim 4, said vapor removing means comprising a conduit extending longitudinally within said drying chamber and communicating therewith through openings spaced along the length thereof.

11. An apparatus for producing carbon-black comprising an inclosed dissociation chamber; means for supplying liquid to said dissociation chamber; arcing electrode means within said dissociation chamber; an inclosed drying chamber; conduit means leading from said dissociation chamber to said drying chamber; means for heating material within said drying chamber; means for removing vapors from said drying chamber; a second inclosed drying chamber; means for delivering material from the firstnamed drying chamber to said second drying chamber; means for heating material within said second drying chamber to a higher temperature than the temperature of heating within the first-named drying chamber; means for removing vapor from said second drying chamber; and means for removing solid material from said second drying chamber.

12. An apparatus as set forth in claim 11, said heating means for the second drying chamber comprising means for heating a gaseous medium and means for passing said gaseous medium through said second drying chamber.

13. An apparatus for producing carbon-black comprising an inclosed dissociation chamber; means for supplying liquid to said dissociation chamber; arcing electrode means within said dissociation chamber; an inclosed drying chamber;

conduit means leading from said dissociation chamber to said drying chamber; means for heating material within said drying chamber; means for removing vapors from said drying chamber; an inclosed cooling chamber; means for delivering solid material from said drying chamber to said cooling chamber; and means for removing heat from material within said cooling chamber.

14. An apparatus as set forth in claim 13, said heat removing means comprising means for passing a gaseous medium at relatively low temperature through said cooling chamber.

15. An apparatus as set forth in claim 13, said heat removing means comprising means for passing a gaseous medium at relatively low temperature. through said cooling chamber, and said apparatus also comprising means for conducting gas irom said cooling chamber and passing the same through said drying chamber.

JOHN J. JAKOSKY. VICTOR, I". HANSON. 

